CN1781379B - Method to increase the foaming capacity of spray-dried powders - Google Patents
Method to increase the foaming capacity of spray-dried powders Download PDFInfo
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- CN1781379B CN1781379B CN2005101038115A CN200510103811A CN1781379B CN 1781379 B CN1781379 B CN 1781379B CN 2005101038115 A CN2005101038115 A CN 2005101038115A CN 200510103811 A CN200510103811 A CN 200510103811A CN 1781379 B CN1781379 B CN 1781379B
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- powder
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- gas
- foam
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- VQHSOMBJVWLPSR-WUJBLJFYSA-N maltitol Chemical compound OC[C@H](O)[C@@H](O)[C@@H]([C@H](O)CO)O[C@H]1O[C@H](CO)[C@@H](O)[C@H](O)[C@H]1O VQHSOMBJVWLPSR-WUJBLJFYSA-N 0.000 description 1
- 229940035436 maltitol Drugs 0.000 description 1
- 229940035034 maltodextrin Drugs 0.000 description 1
- 239000000594 mannitol Substances 0.000 description 1
- 235000010355 mannitol Nutrition 0.000 description 1
- 229960001855 mannitol Drugs 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- HEBKCHPVOIAQTA-UHFFFAOYSA-N meso ribitol Natural products OCC(O)C(O)C(O)CO HEBKCHPVOIAQTA-UHFFFAOYSA-N 0.000 description 1
- 229920000609 methyl cellulose Polymers 0.000 description 1
- 239000001923 methylcellulose Substances 0.000 description 1
- 235000010981 methylcellulose Nutrition 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000004570 mortar (masonry) Substances 0.000 description 1
- 229920001542 oligosaccharide Polymers 0.000 description 1
- 150000002482 oligosaccharides Chemical class 0.000 description 1
- 239000004482 other powder Substances 0.000 description 1
- 235000021485 packed food Nutrition 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 235000013856 polydextrose Nutrition 0.000 description 1
- 239000001259 polydextrose Substances 0.000 description 1
- 229940035035 polydextrose Drugs 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 239000000256 polyoxyethylene sorbitan monolaurate Substances 0.000 description 1
- 235000010486 polyoxyethylene sorbitan monolaurate Nutrition 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 229940068977 polysorbate 20 Drugs 0.000 description 1
- 239000001103 potassium chloride Substances 0.000 description 1
- 235000011164 potassium chloride Nutrition 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- ULWHHBHJGPPBCO-UHFFFAOYSA-N propane-1,1-diol Chemical class CCC(O)O ULWHHBHJGPPBCO-UHFFFAOYSA-N 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 235000020374 simple syrup Nutrition 0.000 description 1
- 235000020183 skimmed milk Nutrition 0.000 description 1
- XDLYMKFUPYZCMA-UHFFFAOYSA-M sodium;4-oct-1-enoxy-4-oxobutanoate Chemical group [Na+].CCCCCCC=COC(=O)CCC([O-])=O XDLYMKFUPYZCMA-UHFFFAOYSA-M 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 235000019710 soybean protein Nutrition 0.000 description 1
- 235000013599 spices Nutrition 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 150000003432 sterols Chemical class 0.000 description 1
- 235000003702 sterols Nutrition 0.000 description 1
- 239000007916 tablet composition Substances 0.000 description 1
- 150000003505 terpenes Chemical class 0.000 description 1
- 235000007586 terpenes Nutrition 0.000 description 1
- 238000012932 thermodynamic analysis Methods 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
- 229920001285 xanthan gum Polymers 0.000 description 1
- 239000000811 xylitol Substances 0.000 description 1
- 235000010447 xylitol Nutrition 0.000 description 1
- HEBKCHPVOIAQTA-SCDXWVJYSA-N xylitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)CO HEBKCHPVOIAQTA-SCDXWVJYSA-N 0.000 description 1
- 229960002675 xylitol Drugs 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING OR TREATMENT THEREOF
- A23C11/00—Milk substitutes, e.g. coffee whitener compositions
- A23C11/02—Milk substitutes, e.g. coffee whitener compositions containing at least one non-milk component as source of fats or proteins
- A23C11/06—Milk substitutes, e.g. coffee whitener compositions containing at least one non-milk component as source of fats or proteins containing non-milk proteins
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING OR TREATMENT THEREOF
- A23C11/00—Milk substitutes, e.g. coffee whitener compositions
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING OR TREATMENT THEREOF
- A23C11/00—Milk substitutes, e.g. coffee whitener compositions
- A23C11/02—Milk substitutes, e.g. coffee whitener compositions containing at least one non-milk component as source of fats or proteins
- A23C11/04—Milk substitutes, e.g. coffee whitener compositions containing at least one non-milk component as source of fats or proteins containing non-milk fats but no non-milk proteins
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23F—COFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
- A23F5/00—Coffee; Coffee substitutes; Preparations thereof
- A23F5/24—Extraction of coffee; Coffee extracts; Making instant coffee
- A23F5/36—Further treatment of dried coffee extract; Preparations produced thereby, e.g. instant coffee
- A23F5/40—Further treatment of dried coffee extract; Preparations produced thereby, e.g. instant coffee using organic additives, e.g. milk, sugar
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23P—SHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
- A23P30/00—Shaping or working of foodstuffs characterised by the process or apparatus
- A23P30/40—Foaming or whipping
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING OR TREATMENT THEREOF
- A23C2240/00—Use or particular additives or ingredients
- A23C2240/20—Inert gas treatment, using, e.g. noble gases or CO2, including CO2 liberated by chemical reaction; Carbonation of milk products
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING OR TREATMENT THEREOF
- A23C2260/00—Particular aspects or types of dairy products
- A23C2260/20—Dry foaming beverage creamer or whitener, e.g. gas injected or containing carbonation or foaming agents, for causing foaming when reconstituted
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Non-Alcoholic Beverages (AREA)
- Tea And Coffee (AREA)
- Glanulating (AREA)
- Manufacturing Of Micro-Capsules (AREA)
- Medicinal Preparation (AREA)
- Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
- Detergent Compositions (AREA)
- Glass Compositions (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Freezing, Cooling And Drying Of Foods (AREA)
- Confectionery (AREA)
Abstract
A method is provided for producing a powdered soluble foaming composition comprising amorphous particles having internal voids filled with atmospheric pressure gas. The method includes subjecting a spray-dried composition to an external pressure and heating the composition at a temperature below the glass transition temperature. The composition is depressurized to result in at least a portion of vacuous internal voids of the composition to be filled with atmospheric pressure gas.
Description
Invention field
The present invention relates to especially, improve the method for spray-dried powders foaming capacity by under the temperature that is lower than the powder glass transition temperature, handling the method that powder improves the powder composition foaming capacity.
Background of invention
The food item that some routines make contains floating foam or foam.For example, cappuccino, milk shake and some soup have floating foam or foam.Some consumers think that the food item that routine makes is preferred, and other consumer day by day need be convenient by the consumer that the fast-food substitute is brought.In order to adapt to consumer's preference, manufacturer has developed fast-food, and it has given the consumer food that they need: have and the fast-food project system of the conventional same or similar feature of food item that makes gets makes things convenient for fast-food by development.The challenge that manufacturer faces is the food that how goes out to have floating foam or foam from the fast-food project construction.
It is earlier previous that to be used for making the solution with floating foam or foam fast-food be the foam powder composition that has produced foam when rebuilding by using in liquid.Used the foaming powder composition to give various Food ﹠ Drink with floating foam or foam characteristic.For example, used composition, foam to give instant cappuccino and other coffee mixture, instant pick-me-up mixture, instant soups mixture, instant milk shake mixture, instant dessert incrustation, instant baste, heat or cold cereal or the like, when Dang Heshui, milk or the mixing of other suitable liquid with floating foam or foam characteristic.
The earlier previous method that is used for making composition, foam is a U.S. Patent No. 6.713,113 provide, it discloses the method for the shape solubility foaming batching that makes powder, batching comprises the matrix that contains carbohydrate, protein and trap gas-pressurized, produces by composition being heated above glass transition temperature.These components are heated above glass transition temperature may cause that outward appearance, local flavor and shelf life to packaged food play the non-oxide browning of side effect (Mei Lade maillard) reaction.
WO2004/019699 discloses the other method that forms composition, foam, wherein protein compositions is accepted gasification under the temperature that is higher than the composition glass transition temperature.Composition, foam preferably contains plasticizer such as carbohydrate polyalcohol or sugar alcohol, and the composition, foam that forms wherein disclosed all use embodiment bases contains the carbohydrate polyalcohol of 5% weight grade.
U.S. Patent Publication No.2003/0026836 discloses the method that forms based on medicine or the food tablet or the powder of carbohydrate, and it comprises accepts tablet or the powder that pressure and the temperature that is higher than glass transition temperature are produced stability when contact with water or dispersed raising with containing the tablet of beverage base-material such as soluble coffee, foam powder, sugar and cream or powder.In addition, disclosed method has promoted the dissolving or the dispersion of tablet or non-foaming powder, is that the dissolving or the dispersion of tablet or powder realizes when tablet or powder being accepted gas-pressurized and make that trap gas wherein promotes to contact with water.The powder that contains protein or the tablet composition that wherein provide all of chemically composited soluble composition embodiment to be based on carbohydrate are provided.Proved the raising that contains trap gas tablet dissolved among the use embodiment therein.Yet, all do not have proof to contain the foaming of trap gas or the dissolving or the dispersed raising of non-foaming powder among any therein use embodiment.
Although there is the method for production foamed product and beverage additive before, still there are the needs of producing the composition, foam method of not having existing method defective.For example, previous method accepts to be higher than the high temperature of glass transition temperature with objective composition, and it causes the composition browning, and produces stink.
Summary of the invention
The method that the present invention relates to change the spray-dried powders structure and therefore improve its foaming capacity, before the inventive method was used, spray-dried powders contained the internal voids to the atmosphere closure of a large amount of sealings.These spaces can hold the gas of enormousness.Yet for the spray-dried powders of the amorphous granular in the sealed inside space of containing the trap atmospheric pressure gas, it also is general also containing gasless basically sealed inside space.Basically gasless sealed inside space is also referred to as vacuum voids at this, thinks that in spray-drying process water evaporates to form from particle.Unfortunately, the existence of vacuum voids has reduced the foaming capacity when spray-dried powders is rebuild in water or other liquid.The application of the inventive method has been opened and has been filled to these vacuum voids of small part with atmospheric pressure gas and advantageously improved the volume that the gas that is held in the powder of foam is provided when rebuilding.In a kind of form, the spray-dried powders that will contain the amorphous granular in sealed inside space is accepted gas-pressurized being lower than under the temperature of glass transition temperature, and decompression makes and is present in opening and be full of atmospheric pressure gas to any vacuum voids of small part in the spray-dried powders then.Although decompression back gas-pressurized does not stop for a long time, improved the foaming capacity of powder as the atmosphere of result's infiltration of the present invention in internal voids.
The method that relates to the powdered soluble composition, foam of making the amorphous granular that contains the internal voids that is full of atmospheric pressure gas in the present invention's one form.This method comprises to be accepted the powdered soluble spray-dried compositions that contains the amorphous granular of vacuum internal voids external pressure and is being lower than heating solubility spray-dried compositions under the temperature of glass transition temperature.Therefore cause the internal voids of partial vacuum at least of composition to be full of atmospheric pressure gas the composition decompression.
In the multiple further form, spray-dried compositions is no protein compositions, carbohydrate-free compositions, protein compositions, or carbohydrate composition.Spray-dried compositions can comprise for example emulsifying agent of dispersed fat, surfactant arbitrarily, or buffer salt for example.In the further interchangeable form, the amount that composition contains atmospheric pressure gas is enough to make every gram composition, foam to discharge at least about 2cc gas, and the about 5cc gas of preferably every at least gram composition, foam is when being dissolved in the water under environmental condition.Make spray-dried compositions by any spray drying process known in the art, include, but are not limited to jet and non-jet spray drying technology.
DESCRIPTION OF THE PREFERRED
The present invention relates to contain the foam powder composition that is full of the atmospheric pressure gas internal voids, the spray-dried compositions that the method for use wherein will contain the amorphous granular of sealed inside vacuum voids is accepted external pressure and is heated being lower than under the temperature of glass transition temperature.This method causes big impervious and is full of the space of powder.
The batching that can be used for preparing no protein powder comprises carbohydrate, lipid and other no protein material.Carbohydrate is preferred and include but not limited to sugar, polyhydroxy-alcohol, sugar alcohol, oligosaccharides, polysaccharide, starch hydrolysate, colloid, Soluble Fiber, modified starch and modified cellulose.Suitable steamed bun stuffed with sugar is drawn together glucose, fructose, sucrose, lactose, mannose and maltose.Suitable polyhydroxy-alcohol comprises glycerine, propane diols, polyglycereol and polyethylene glycol.Suitable sugar alcohol comprises D-sorbite, mannitol, maltitol, lactitol, antierythrite and xylitol.Suitable starch hydrolysate comprises maltodextrin, dextrose syrup, corn syrup, high malt sugar syrup and high fructose syrup.Suitable colloid comprises xanthans, alginates, carragheen, guar gum, gellan gum, locust tree beanpod glue and hydrolysis colloid.Suitable Soluble Fiber comprises inulin, hydrolysis guar gum and polydextrose.Suitable modified starch comprises and dissolves in or be scattered in physics or converted starch in the water.Suitable modified cellulose comprises methylcellulose, carboxymethyl cellulose and HPMC.
Can be used for the composition of formulate carbohydrate-free powders comprises protein, lipid and other carbohydrate material.Protein is preferred and include, but are not limited to milk protein, soybean protein, egg albumen, gelatin, collagen, wheat gluten and protein hydrolysate.Suitable protein hydrolysate comprises gelatin hydrolysate, hydrolytic collagen matter, caseinhydrolysate, hydrolyzing lactoalbumin, hydrolyzed milk protein, hydrolytic soya bean protein, hydrolysis egg albumen, hydrolyzed wheat protein and amino acid.The food composition of not having protein and carbohydrate simultaneously can be used for preparing the new varieties powder, can include, but are not limited to organic and inorganic salts, surfactant, emulsifying agent, plant compound, nourishing additive agent, flowing activity agent, artificial sweetener, anticorrisive agent, pigment and some spices.That lipid includes, but are not limited to is plant-derived, fat, oil, hydrogenated oil and fat, ester-exchanged oil, phosphatide, wax, sterol, stanols, terpenes and the aliphatic acid of dairy products or animal origin.
Perhaps, the inventive method can use above-mentioned carbohydrate and protein to be used for comprising simultaneously the powder of carbohydrate and protein.In addition, powder can be dry soluble coffee extract.Can produce powdered soluble composition, foam of the present invention by any method that the grain structure with a plurality of internal voids that can keep gas effectively is provided.The jet spray-drying of the conventional aqueous solution is to produce the method for optimizing of these powdered soluble composition, foams, but not having jet aqueous solution spray-drying also is suitable method.Do not have jet spray-drying and produce particle usually, but this less preferable methods also can be used to make no protein, carbohydrate and other powder with suitable internal void volumes with relatively little internal void volume.Preferred nitrogen, jet but any other food-grade gas can be used for, comprise air, carbon dioxide, nitrous oxide or its mixture.
Randomly use one or more surfactants to prepare composition, foam of the present invention and improve that bubble in spray-drying process forms and the formation of internal voids.The suitable surfactant of use appropriate amount can be used for influencing relative size, quantity and the volume of internal voids.Because most of food proteins are self-faced activity, can need surfactant and produce many suitable carbohydrate-free compositions that contain protein that have suitable internal void volumes.Yet, have been found that the manufacturing of using surfactant greatly to improve no protein compositions.Surfactant comprises the diacetyl tartrate of the emulsifying agent of food permission such as polysorbate, sucrose ester, stearyl lactylic acid salt, monoglyceride/diglyceride, monoglyceride/diglyceride, and phosphatide.Some carbohydrate are surface-active, can be used in combination with other carbohydrate and prepare no protein compositions.Suitable surface-active carbohydrate comprises the starch that Arabic gum, propylene glycol alginate and lipophilicity modified food starch such as octenyl succinate replace.
The preparation that the present invention is based on the protein composition, foam uses one or more buffers can be with helping spray-drying and rebuilding in liquid.Use the suitable buffer of appropriate amount can be used to provide suitable granule interior voidage and improve powder dissolution and product foam characteristics.The used preferred reducing of the present invention is the salt of organic or inorganic acid.Except the benefit of having mentioned is provided, during these buffers have also improved in some product is used as acidic beverages to protein aggegation or rotten resistance.Most preferred buffer is organic acid sodium salt and sylvite.Suitable reducing includes, but are not limited to sodium, potassium, calcium and the magnesium salts of citric acid, malic acid, fumaric acid and phosphoric acid.
The powder that is used for making composition, foam of the present invention bulk density (bulkdensity) and tap density (tap density) before accepting external pressure are 0.1-0.7g/cc, be generally 0.2-0.6g/cc, skeletal density is 0.3-1.6g/cc, be generally 0.4-1.5g/cc, real density is 1.2-1.6g/cc, internal void volume is 5-80%, usually 10-75%.Owing to keep the ability of gas bigger, usually the powder that preferably has big relatively internal void volume.Suitable internal void volume is at least about 10%, preferably at least about 30%, more preferably at least about 50%.The glass transition temperature of powder is 30-150 ℃, is generally 40-125 ℃, is more typically 50-100 ℃.The powder moisture is 0-15%'s, common 1-10%, and more generally 2-5% and water activity are 0-0.5, usually 0.05-0.4, more generally 0.1-0.3.
Term " trap gas " meaning is to be present in the mealy structure internal voids and not open the gas that mealy structure can not leave this structure.Term " gas of the maintenance " meaning be present in the mealy structure internal voids and the change of response external air pressure or gas composition as can enter and leave the gas of this structure by crack or other opening.Preferably, according to embodiment of the present invention, after applying and discharging external pressure, the gas that great majority are present in the powder is that physics remains in the powder internal voids that is connected with atmosphere.Gas that can suitable use according to the present invention is selected from nitrogen, carbon dioxide, nitrous oxide, air or its mixture.Preferred nitrogen, but can use any other food-grade gas that external pressure is used to powder.
Term " structure ", " micrograined texture ", " grain structure " or " mealy structure " meaning are to contain a large amount of sealed inside spaces to the atmosphere closure, a large amount of internal voids to atmosphere opening, or the structure of its combination.These spaces can keep a large amount of gases, discharge and the generation foam as bubble when structure is dissolved in the liquid.Term " amorphous " meaning is to be mainly non-crystal glassy structure.
Term " powdered soluble composition, foam ", " foam powder composition " or " composition, foam " meaning is any powder of formation foam or floating foam can be dissolved or dispersed in liquid and especially contact in the aqueous liquid and with such liquid the time.
Percentage is based on the weight of composition, foam, unless otherwise noted.
It is any carbohydrate or the protein compatible with powder final use of the present invention that term " carbohydrate " and " protein " look like separately.This looks like in practice is to be suitable for consumption.
Term " emulsifying agent " meaning is compatible with powder final use of the present invention to have oil or gas emulsification property and any surface active cpd that be not protein.
By measure the volume (cc) that when pouring in the graduated cylinder by passage, occupies of the powder of the weight of giving (g) come bulk density (g/cc).By powder is poured in the graduated cylinder, vibrating barrel until powder sink down into minimum volume, recording volume, the powder and weight measured bulk density (g/cc) divided by volume of weighing.By using helium specific gravity bottle (Micromeritics AccuPyc1330) to measure to have weighed the volume of powder and weight being measured skeletal density (g/cc) divided by volume.Skeletal density is the measurement of density, comprises any volume to the atmospheric sealing space that is present in the particle, gets rid of gap between particles volume and any volume to the atmosphere opening space that is present in the particle.Also be derived from the skeletal density of removing or after atmosphere is opened all internal voids, measuring powder grinding with mortar and pestle at this volume that is called the sealed airspace of internal voids.In this type skeletal density that is called real density (g/cc), only be the actual density that constitutes this powdered solid substance.The inverse (cc/g) that deducts real density by the inverse (cc/g) with skeletal density multiply by this difference skeletal density (cc/g) and 100% then and records internal void volume (%), i.e. sealed inside voidage % in comprising particles of powder.
Glass transition temperature sign second-order phase transistion is characterized by powder composition and changes into the softened rubber attitude from hard glassy state.Usually, or to be higher than under the glass transition temperature gas dissolution rate in the material and diffusivity all higher.Glass transition temperature depends on chemical composition and moisture, and usually, lower mean molecule quantity and/or higher moisture will reduce glass transition temperature.Use any appropriate method well known by persons skilled in the art to improve or reduce glass transition temperature consciously by the moisture that reduces or increase powder separately simply.Can use existing differential scanning calorimetry or thermodynamic analysis technology to measure glass transition temperature.
Can make the present invention and contain the new composition, foam that keeps atmospheric pressure gas by in any convenient pressure container, under pressure, any spray-dried powders being heated to the temperature that is lower than glass transition temperature and powder being cooled off by quick release pressure or by cooled containers before decompression, appended powder include, but are not limited to based on protein powder, based on the powder of carbohydrate, based on powder or its mixture of soluble coffee, they have the suitable grain structure that contains the sealed inside vacuum voids.A method is that powder-tight is pressurizeed in pressure vessel and with Compressed Gas, then in thermostat by being positioned over preheating or the water bath or cycle through inner coil pipe or overcoat by electric current or hot fluid and come heated pressure container a period of time to come effectively gas-pressurized to be full of internal voids in the particle with the temperature that improves powder, but do not reach or be higher than glass transition temperature, then by being positioned in the water bath or being cooled to about room temperature by the still container of pressurization that the cold fluid circulation will contain powder, release pressure and open container and collect composition, foam then.Method for optimizing is powder to be carried out gas pressurized and decompression in the pressure vessel of environment temperature and do not have external heat or cooling.Can make and produce composition, foam in any suitable manner in batches or continuously.
Usually, at 5-70 ℃, preferred 20-60 ℃, more preferably 25-40 ℃ of heating powder 1-1000 second, preferred 5-600 second, more preferably 60-300 second.Pressure in the pressure vessel is 100-3000psi, preferred 200-2000psi, more preferably 500-1500psi.Preferred use nitrogen, but any other food-grade gas can be used for pressurizing vessel, comprises air, carbon dioxide, nitrous oxide or its mixture.Powder gas content and foaming capacity increase along with processing pressure usually.The reset pressure that heating can cause being sent in the pressure vessel significantly improves.Reset pressure be multiply by the recently approximate maximum pressure that pressure vessel inside reaches in heating process, wherein the temperature use kelvin degree unit of obtaining of heating-up temperature and original temperature.For example, container is forced into 1000psi, is heated to 70 ℃ (343K) then and the pressure in the pressure vessel can be increased to about 1150psi at 25 ℃ (298K).The resulting foam powder composition that contains the trap gas-pressurized has about 1 to 5000 micron particle diameter usually, and about 5 to 2000 microns usually, more generally about 10 to 1000 microns.
Usually the degree that open in the sealed inside space in the powder is along with adding external pressure and time and increasing, and relatively high pressure can be used for improving validity and shortening the processing time.When gasifying under optimum condition, the distribution of the particle diameter of powder is free burial ground for the destitute change intentionally usually.Believe in the glassy state amorphous granular that the external pressure that applies contains in powder to form stress crack, the internal voids that it opens to the small part sealing, make at least the partial vacuum space is full of atmospheric pressure gas when externally air pressure discharges.
Under being lower than glass transition temperature with powder pressurization and when going to press, the blink after going to press in the section these particles to produce faint explosion sound be common.By being lower than the pressurization under the glass transition temperature, powder outward appearance and bulk density significantly do not change usually, but skeletal density, internal void volume and maintenance gas content have significantly changed usually.
When the appropriate protection of using antagonism moisture to invade under being lower than glass transition temperature was stored, the powder with good stability kept structure, internal void volume and the maintenance gas content of their changes.It is functional many months backs usually to be stored under the room temperature powder in the closed container.Be lower than the powder that pressurizes under the gamma transition attitude temperature and gas-pressurized do not kept long-time section.Yet, be surprisingly found out that the spray-dried powders that pressurizes under the gamma transition attitude temperature being lower than, usually produce remarkable foam of Duoing even lose the back than pressurized powder not at gas-pressurized.The useful increase of believing this foaming capacity be infiltrate through by atmospheric pressure gas before in the dry run water from particle, evaporate in the vacuum internal voids that forms and cause.Remarkable effect can at room temperature be carried out and bring to the new method that has been found that this raising spray-drying composition, foam foaming capacity.
The preferable use of these new composition, foams is in soluble beverage mixture especially instant coffee and cappuccino mixture.Yet they can be used for any fast-food with the liquid rehydration.Although these composition, foams are dissolved in well in the cold liquid usually and produce foam, in hot liquid, rebuild usually and improved dissolving and foaming capacity.Application comprises instant beverage, dessert, cheese powder, cereal, soup, surface decoration powder and other products.
The embodiment that below comprises provides the present invention further to understand, but limits the scope of the invention anything but.
Embodiment 1: 50% aqueous solution of the starch (8% based on dry weight) that 33DE dextrose syrup solid (92% based on dry weight) and octenyl succinate are replaced produces the no protein powder that comprises the amorphous granular with a large amount of internal voids with nitrogen jet and spray-drying.Basically 100% carbohydrate powder is a white, and bulk density is 0.25g/cc, and tap density is 0.31g/cc, and skeletal density is 0.59g/cc, and internal void volume is 61%, and real density is 1.51g/cc, T
gBe 74 ℃, moisture about 2%.In instant sweet coffee mixture, use powder, use about three parts of powder to the weight ratio of a soluble coffee to two portions of sugar, when using 130ml88 ℃ of water will about 11g mixture to rebuild in the 250ml of 65mm internal diameter beaker, the foam volume of generation covers the height of the surface of beverage to about 7mm fully.
At 25 ℃ of (stainless steel gas sampling cylinders of 75cc capacity in pressure vessel; Make by WhiteyCorporation; Be used for all embodiment at this) with 1000psi nitrogen 6g there are not protein powder pressurization 5 minutes, decompression then.Untreated powder with waiting in the alternative sweet coffee mixture of heavy processing powder has shown the powder foam ability about 140% that improved of handling.To handling and the understanding of the foam volume of the foam density of the reconstruction beverage mix that untreated powder causes and increase is used for estimating the gas flow (proofreading and correct to room temperature and room pressure) of every kind of powder release.Estimate that the every gram powder of untreated powder discharges about 2cc gas, discharges about 5cc gas and handle the every gram powder of powder.Powder produces slight explosion sound in short time after decompression, may be the explosion owing to diffusion-restriction clearance gap surrounding wall, too easily breaks so that can not contain gas-pressurized in the space.The bulk density of handling powder does not change, but skeletal density is increased to 0.89g/cc, internal void volume is reduced to 41%, has shown that vacuum internal voids that the power of pressurization and/or decompression form before will part has been opened to atmosphere to improve foaming capacity in the particle dehydration.This hypothesis obtains true support: even after a week, the powder of processing still keeps the foaming capacity that improves.
Embodiment 2: 50% aqueous solution of 33DE dextrose syrup solid (98.5% based on dry weight), polysorbate 20 (1% based on dry weight) and propylene glycol alginate (0.5% based on dry weight) is produced the no protein powder that comprises the amorphous granular with a large amount of internal voids with nitrogen jet and spray-drying.About 99% carbohydrate powder is a white, and bulk density is 0.24g/cc, and tap density is 0.30g/cc, and skeletal density is 0.64g/cc, and internal void volume is 56%, and real density is 1.47g/cc, T
gBe 68 ℃, moisture about 4%.Method according to embodiment 1 is used powder in the sweet coffee mixture, when using 130ml88 ℃ of water will about 11g mixture to rebuild in the 250ml of 65mm internal diameter beaker, the foam volume of generation covers the height of the surface of beverage to about 11mm fully.
In pressure vessel, 6g there are not protein powder pressurization 5 minutes, decompression then at 25 ℃ with 1000psi nitrogen.Untreated powder with waiting in the alternative sweet coffee mixture of heavy processing powder has shown the powder foam ability about 65% that improved of handling.To handling and the understanding of the foam volume of the foam density of the reconstruction beverage mix that untreated powder causes and increase is used for estimating the gas flow (proofreading and correct to room temperature and room pressure) of every kind of powder release.Be estimated as the every gram powder of untreated powder and discharge about 3.5cc gas, discharge about 6cc gas and handle the every gram powder of powder.Powder produces slight explosion sound in short time after decompression.The bulk density of handling powder does not change, but skeletal density increases to 1.04g/cc, internal void volume is reduced to 29%, has shown that vacuum internal voids that the power of pressurization and/or decompression form before will part has been opened to atmosphere to improve foaming capacity in the particle dehydration.This hypothesis obtains true support: even after a week, the powder of processing still keeps the foaming capacity that improves.
Embodiment 3: when the spray-drying of other 6g embodiment 1 do not have the protein powder sample according to the method for embodiment 1 when pressurizeing under following time of listing and pressure with nitrogen for 25 ℃, wherein the method according to embodiment 1 will wait the untreated powder of heavily handling in the alternative sweet coffee mixture of powder, and following table 1 has been summed up the result who obtains.Untreated prods is the untreated powder of embodiment 1 and is included in and is used for comparison in the table.Product A and B are other untreated powder samples of pressurization different time under 250psi; Products C is another untreated powder sample in the 375psi pressurization; Product D is another untreated powder sample in the 500psi pressurization; With product E be another untreated powder sample in 750psi pressurization.Product F is embodiment 1 powder that pressurizes under 1000psi and is included in and is used for comparison in the table.Product G adds pressure ratio product F another untreated powder sample of longer time under 1000psi.Pressurizeed down only 5 minutes with respect to 250psi as can be seen, pressurization only slightly improved foaming capacity in 30 minutes under 250psi.In 375psi, 500psi, 750psi or 1000psi pressurization further do not improve pressurization in 30 minutes 5 minutes the foaming capacity of corresponding powder only.
Table 1
| Product | Pressure (psi) | Time (minute) | The increase % of foam height (in the 250ml beaker) in the coffee mixture | The gas that from composition, foam, discharges (cc gas/g powder) of estimation |
| Be untreated | - | - | - | 2 |
| A | 250 | 5 | 0 | 2 |
| B | 250 | 30 | 30 | 3 |
| C | 375 | 5 | 30 | 3 |
| D | 500 | 5 | 55 | 4 |
| E | 750 | 5 | 100 | 5 |
| F | 1000 | 5 | 100 | 5 |
| G | 1000 | 30 | 100 | 5 |
Embodiment 4: do not have the protein powder sample when the spray-drying of other 6g embodiment 2 and under the following pressure of listing, pressurize 5 minutes the time with nitrogen at 25 ℃ according to the method for embodiment 1, wherein will wait when heavily handling powder and substituting untreated powder in the sweet coffee mixture according to the method for embodiment 1, following table 2 has been summed up the result who obtains.Untreated prods is the untreated powder of embodiment 2 and is included in and is used for comparison in the table.Product A is another untreated powder sample that pressurizes under 250psi; Product B is another untreated powder sample that pressurizes under 375psi; Products C is another untreated powder sample in the 500psi pressurization; Product D is another untreated powder sample in the 750psi pressurization.Product E is embodiment 2 powder that pressurize under 1000psi and is included in and is used for comparison in the table.Product F adds pressure ratio product E another untreated powder sample of longer time under 1250psi.In further do not improve under 250psi or 1000psi pressurization in 30 minutes 5 minutes the foaming capacity of corresponding powder only of pressurization under 250psi or the 1000psi.Find to increase pressure and increased skeletal density gradually, by may having opened the vacuum internal voids before more most of, it has reduced the cumulative volume of residual internal voids and has improved the foaming capacity of powder.Do not influence the bulk density of powder by pressure treatment.
Table 2
| Product | Pressure (psi) | Internal void volume (%) | The increase % of foam height (in the 250ml beaker) in the coffee mixture | The gas that from composition, foam, discharges (cc gas/g powder) of estimation |
| Be untreated | - | 56 | - | 3.5 |
| A | 250 | 42 | 0 | 3.5 |
| B | 375 | 39 | 15 | 4.5 |
| C | 500 | 37 | 25 | 5 |
| D | 750 | 33 | 55 | 6 |
| E | 1000 | 29 | 55 | 6 |
| F | 1250 | 28 | 55 | 6 |
Embodiment 5: 50% aqueous solution of 33DE dextrose syrup solid (52% based on dry weight), skimmed milk power (47% based on dry weight) and disodium hydrogen phosphate (1% based on dry weight) is produced the powder that contains carbohydrate and protein with nitrogen jet and spray-drying.White powder has the amorphous granular structure, milk smell, and bulk density is 0.34g/cc, and tap density is 0.40g/cc, and skeletal density is 0.71g/cc, and internal void volume is 52%, real density is 1.49g/cc, T
gBe 61 ℃, moisture about 3%.Use powder according to embodiment 1 method in the sweet coffee mixture, when will about 11g mixture with 130ml88 ℃ of water rebuilding in the 250ml of 65mm internal diameter beaker, the foam volume of generation covers the height of the surface of beverage to about 10mm fully.
With 1000psi nitrogen the powder that 6g contains carbohydrate and protein was pressurizeed 5 minutes in pressure vessel at 25 ℃, then decompression.Untreated powder with waiting in the alternative sweet coffee mixture of heavy processing powder has shown the powder foam ability about 160% that improved of handling.To handling and the understanding of the foam volume of the foam density of the reconstruction beverage mix that untreated powder causes and increase is used for estimating the gas flow (proofreading and correct to room temperature and room pressure) of every kind of powder release.Estimate that the every gram powder of untreated powder discharges about 3.5cc gas, discharges about 8.5cc gas and handle the every gram powder of powder.Powder produces slight explosion sound in short time after decompression.The bulk density of handling powder does not change, it is 0.75g/cc that but skeletal density increases, internal void volume is reduced to 50%, has shown that vacuum internal voids that the power of pressurization and/or decompression form before will part has been opened to atmosphere to improve foaming capacity in the particle dehydration.This hypothesis obtains true support: even after a week, the powder of processing still keeps the foaming capacity that improves.
Embodiment 6: obtain commercial carbohydrate gelatin hydrolysate powder, do not produce by there being jet spray drying aqueous solution.99.2% has the amorphous granular structure based on the dry weight protein powder, and faint yellow, bulk density is 0.45g/cc, and tap density is 0.54g/cc, and skeletal density is 1.15g/cc, and internal void volume is 18%, and real density is 1.41g/cc, T
gBe 80 ℃, moisture about 6%.Powder is added in the instant cappuccino mixture, use about 1 part of powder to a soluble coffee to the weight ratio of two portions of sugar to three parts of foaming creams.When will about 13g cappuccino mixture rebuilding in the 250ml of 65mm internal diameter beaker with 130ml88 ℃, the foam volume of generation covers the height of the surface of beverage to about 14mm fully.
With 1000psi nitrogen the 6g carbohydrate-free powder was pressurizeed 5 minutes in pressure vessel at 25 ℃, then decompression.Untreated powder with waiting in the alternative cappuccino mixture of heavy processing powder has shown the powder foam ability about 150% that improved of handling.To handling and the understanding of the foam volume of the foam density of the reconstruction beverage mix that untreated powder causes and increase is used for estimating the gas flow (proofreading and correct to room temperature and room pressure) of every kind of powder release.Estimate that the every gram powder of untreated powder discharges about 2cc gas, discharges about 5.5cc gas and handle the every gram powder of powder.Powder produces slight explosion sound in short time after decompression.The bulk density of handling powder does not change, it is 1.24g/cc that but skeletal density increases, internal void volume is reduced to 12%, has shown that vacuum internal voids that the power of pressurization and/or decompression form before will part has been opened to atmosphere to improve foaming capacity in the particle dehydration.This hypothesis obtains true support: even after a week, the powder of processing still keeps the foaming capacity that improves.
Embodiment 7: 33DE dextrose syrup solid (82% based on dry weight) and surface-active sodium octenyl succinate substituted starch (8% based on dry weight) and 50% aqueous solution that contains the dispersion emulsion (10% based on dry weight) of partially hydrogenated soybean oil are produced the no protein powder that comprises the amorphous granular with a large amount of internal voids with nitrogen jet and spray-drying.The powder of about 90% carbohydrate is a white, and bulk density is 0.21g/cc, and tap density is 0.26g/cc, and skeletal density is 0.52g/cc, and internal void volume is 64%, and real density is 1.44g/cc, T
gBe 65 ℃, moisture about 3%.Method according to embodiment 1 is used for the sweet coffee mixture with powder, and when will about 11g mixture with 130ml88 ℃ of water rebuilding in the 250ml of 65mm internal diameter beaker, the foam volume of generation covers the height of the surface of beverage to about 10mm fully.
In pressure vessel, 6g there are not protein powder pressurization 5 minutes, decompression then at 25 ℃ with 1000psi nitrogen.Untreated powder with waiting in the alternative sweet coffee mixture of heavy processing powder has shown the powder foam ability about 100% that improved of handling.To handling and the understanding of the foam volume of the foam density of the reconstruction beverage mix that untreated powder causes and increase is used for estimating the gas flow (proofreading and correct to room temperature and room pressure) of every kind of powder release.Estimate that the every gram powder of untreated powder discharges about 3.5cc gas, discharges about 6.5cc gas and handle the every gram powder of powder.Powder produces slight explosion sound in short time after decompression, may be the explosion owing to diffusion-restriction clearance gap surrounding wall, too easily breaks so that can not contain gas-pressurized in the space.The bulk density of handling powder does not change, it is 0.64g/cc that but skeletal density increases, internal void volume is reduced to 56%, has shown that vacuum internal voids that the power of pressurization and/or decompression form before will part has been opened to atmosphere to improve foaming capacity in the particle dehydration.
Embodiment 8: according to U.S. Patent No. 5,882, spray-drying espresso powder is made in 717 instruction.Powder has the amorphous granular structure, and bulk density is 0.19g/cc, and tap density is 0.22g/cc, and skeletal density is 0.72g/cc, and internal void volume is 51%, and real density is 1.47g/cc, T
gIt is 74 ℃.Use powder in the instant cappuccino mixture of embodiment 7, when will about 11g cappuccino mixture with 130ml88 ℃ of water rebuilding in the 250ml beaker, the foam volume of generation covers the height of the surface of beverage to about 14mm fully.
With 1000psi nitrogen the 5g powder was pressurizeed 5 minutes in pressure vessel at 25 ℃, then decompression.Untreated powder with waiting in the alternative cappuccino mixture of heavy processing powder has shown the powder foam ability about 65% that improved of handling.To handling and the understanding of the foam volume of the foam density of the reconstruction beverage mix that untreated powder causes and increase is used for estimating the gas flow (proofreading and correct to room temperature and room pressure) of every kind of powder release.The every gram coffee of coffee powder of estimating to be untreated discharges about 4cc gas, discharges about 6.5cc gas and handle the every gram coffee of coffee powder.Powder produces slight explosion sound in short time after decompression.The bulk density of handling powder does not change, it is 1.35g/cc that but skeletal density increases, internal void volume is reduced to 8%, has shown that vacuum internal voids that the power of pressurization and/or decompression form before will part has been opened to atmosphere to improve foaming capacity in the particle dehydration.
Although described in detail the present invention with reference to preferred embodiment, be clear that the present invention can make multiple change and variation, be conspicuous to those skilled in the art, and do not deviate from the spirit and scope of the present invention.
Claims (35)
1. comprise the manufacture method of the powdered soluble composition, foam of the amorphous granular with the internal voids that is full of atmospheric pressure gas, described method comprises:
External pressure is applied to the powdered soluble spray-dried compositions that comprises amorphous granular with vacuum internal voids;
Be lower than heating solubility spray-dried compositions under the temperature of glass transition temperature; With
Therefore cause the internal voids of partial vacuum at least of composition to be full of atmospheric pressure gas the composition decompression.
2. the process of claim 1 wherein that external pressure is 200psi at least.
3. the process of claim 1 wherein that described external pressure is 500psi at least.
4. the process of claim 1 wherein that described external pressure is 1000psi at least.
5. the process of claim 1 wherein that described external pressure applied for 1 second at least.
6. the process of claim 1 wherein that described external pressure applies 1 minute at least.
7. the process of claim 1 wherein and be used for causing the gas of described external pressure to be selected from air, nitrogen, carbon dioxide, nitrous oxide and composition thereof.
8. the process of claim 1 wherein that described spray-dired composition is protein-free.
9. the method for claim 8, wherein said spray-dired composition contains dispersed fat.
10. the method for claim 8, wherein said spray-dired composition contains carbohydrate.
11. the method for claim 10, wherein said spray-dired composition further contains surfactant.
12. the method for claim 11, wherein said surfactant is an emulsifying agent.
13. the method for claim 12, wherein said emulsifying agent are selected from diacetyl tartrate, phosphatide, propylene glycol alginate, lipophilicity modified starch or its mixture of polysorbate, sucrose ester, stearyl lactylic acid salt, monoglyceride/diglyceride, monoglyceride/diglyceride.
14. the process of claim 1 wherein that described spray-dired composition is a carbohydrate.
15. the method for claim 14, wherein said spray-dired composition contains protein.
16. the method for claim 14, wherein said spray-dired composition contains dispersed fat.
17. the method for claim 14, wherein said spray-dired composition further contains buffer.
18. the method for claim 17, wherein said buffer are the salt of organic or inorganic acid.
19. the method for claim 18, wherein said salt are selected from sodium, potassium, magnesium or the calcium salt of citric acid, fumaric acid, malic acid, phosphoric acid or its mixture.
20. the process of claim 1 wherein that described spray-dired composition contains dispersed fat.
21. the process of claim 1 wherein that described composition had at least 10% internal void volume before accepting external pressure.
22. the process of claim 1 wherein that described particle had at least 30% internal void volume before accepting external pressure.
23. the process of claim 1 wherein that described particle had at least 50% internal void volume before accepting external pressure.
24. the process of claim 1 wherein when amount that described composition contains atmospheric pressure gas is dissolved in liquid under environmental condition, be enough to make the described composition, foam of every gram to discharge 2cc gas at least.
25. the process of claim 1 wherein when amount that described composition contains atmospheric pressure gas is dissolved in liquid under environmental condition, be enough to make the described composition, foam of every gram to discharge 5cc gas at least.
26. the method for claim 1 further comprises the solubility spray-dried compositions from being lower than the heating-up temperature cooling of glass transition temperature.
27. the method for claim 26 is wherein carried out described cooling before the composition decompression.
28. the method for claim 26 is wherein carried out described cooling when composition reduces pressure.
29. the method for claim 26, wherein said cooling comprise composition is cooled to room temperature from the heating-up temperature that is lower than glass transition temperature.
30. the process of claim 1 wherein and when heating combination, carry out the described external pressure that applies.
31. the process of claim 1 wherein and before external pressure is applied to composition, carry out described heating.
32. the process of claim 1 wherein that described spray-dried compositions forms by the dry aqueous solution of gas spraying.
33. the method for claim 1 comprises further that the dry aqueous solution of gas spraying forms and has the grains of composition with internal voids.
34. the method for claim 33, used gas is selected from air, nitrogen, carbon dioxide, nitrous oxide and composition thereof in the wherein said gas spraying drying.
35. the method for claim 1 comprises further that the dry aqueous solution of non-pneumatic spraying forms and has the grains of composition with internal voids.
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| US10/919474 | 2004-08-17 | ||
| US10/919,474 US7736683B2 (en) | 2004-08-17 | 2004-08-17 | Method to increase the foaming capacity of spray-dried powders |
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| CN1781379B true CN1781379B (en) | 2010-09-29 |
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